simulation repor1 lab 3

Simulation Report

File Name: New ProjectCompany:Customer:Project:Job No:Prepared By:Report Date: 10/22/2015 10:37:20 AMUnit Set: Field

File: New Project.vmpiCON v8.0

Main Flowsheet....................................................................................................................................................3Material Streams.............................................................................................................................................3Energy Streams...............................................................................................................................................9Conv Reactors...............................................................................................................................................11Coolers............................................................................................................................................................13Heaters.............................................................................................................................................................14Separators......................................................................................................................................................15

*Bold face throughout the report denotes specified values.*Italic face throughout the report denotes recycle values.

Customer: JobNo: Project:

Prepared by:

RootThermo (Thermodynamic Model)

Main Data

Property Package Name Advanced_Peng-Robinson Compound Count 3

Compounds

n-HEPTANE TOLUENE HYDROGEN

File: New Project.vmpApril-21-23 iCON v8.0 of 15


Prepared by:

/stream_A (Material Stream)

Prop Pkg: Advanced Peng-Robinson

Connections

Material Inlets

Connection Up Stream Unit OpIn ---- ----

Material Outlets

Connection Down Stream Unit OpOut heater ----

Natural Gas / Component Content

Water [lb/MMSCF] 0.00 Sulfur (Total) [grain/100SCF] 0.00Mercaptans [grain/100SCF] 0.00 H2S [grain/100SCF] 0.00CO2 [Fraction] 0.00 N2 [Fraction] 0.00H2 [ppm] 0.00 O2 [ppm] 0.00

Settings / Eq. Results Configuration

Include Bulk Liq. in Eq. Results False View Component Free Compositions FalseName for Component Free Cmp. Free Exclude from Component Free

n-HEPTANE 0.00 TOLUENE 0.00 HYDROGEN 0.00

Equilibrium Results

Bulk Vapour Liquid01.00 0.00 1.00

T [F] 65.00 65.00 65.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 100.00 0.00 100.00Mass Flow [lb/h] 10020.19 0.00 10020.19Mole Fraction [Fraction] n-HEPTANE 1.00 1.00 1.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00Mass Fraction [Fraction] n-HEPTANE 1.00 1.00 1.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00MoleFlows [lbmol/h] n-HEPTANE 100.00 0.00 100.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00MassFlows [lb/h] n-HEPTANE 10020.19 0.00 10020.19 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00



Prepared by:

/stream_B (Material Stream)


Connections

Material Inlets

Connection Up Stream Unit OpIn heater ----

Material Outlets

Connection Down Stream Unit OpOut catalytic_reactor ----






Equilibrium Results





Prepared by:

/stream_C (Material Stream)


Connections

Material Inlets

Connection Up Stream Unit OpIn catalytic_reactor ----

Material Outlets

Connection Down Stream Unit OpOut cooler ----


Water [lb/MMSCF] 0.00 Sulfur (Total) [grain/100SCF] 0.00Mercaptans [grain/100SCF] 0.00 H2S [grain/100SCF] 0.00CO2 [Fraction] 0.00 N2 [Fraction] 0.00H2 [ppm] 3.75E+05 O2 [ppm] 0.00E+00



n-HEPTANE 0.00E+00 TOLUENE 0.00E+00 HYDROGEN 0.00E+00

Equilibrium Results





Prepared by:

/stream_D (Material Stream)


Connections

Material Inlets

Connection Up Stream Unit OpIn cooler ----

Material Outlets

Connection Down Stream Unit OpOut separator ----






Equilibrium Results





Prepared by:

/stream_E (Material Stream)


Connections

Material Inlets

Connection Up Stream Unit OpIn separator ----

Material Outlets

Connection Down Stream Unit OpOut ---- ----






Equilibrium Results





Prepared by:

/stream_F (Material Stream)


Connections

Material Inlets

Connection Up Stream Unit OpIn separator ----

Material Outlets

Connection Down Stream Unit OpOut ---- ----






Equilibrium Results


T [F] 65.00 65.00 65.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 97.35 0.00 97.35Mass Flow [lb/h] 9631.43 0.00 9631.43Mole Fraction [Fraction] n-HEPTANE 0.8488 0.0378 0.8488 TOLUENE 0.1507 0.0053 0.1507 HYDROGEN 5.18E-04 9.57E-01 5.18E-04Mass Fraction [Fraction] n-HEPTANE 0.8597 0.6106 0.8597 TOLUENE 0.1403 0.0785 0.1403 HYDROGEN 1.06E-05 3.11E-01 1.06E-05MoleFlows [lbmol/h] n-HEPTANE 82.63 0.00 82.63 TOLUENE 14.67 0.00 14.67 HYDROGEN 0.05 0.00 0.05MassFlows [lb/h] n-HEPTANE 8279.78 0.00 8279.78 TOLUENE 1351.54 0.00 1351.54 HYDROGEN 0.10 0.00 0.10



Prepared by:

/Q-1 (Energy Stream)


Connections

Energy Streams

Connection ValueIn [Btu/h] ---- 5884805.6004Out [Btu/h] /heater.InQ 5884805.6004



Prepared by:

/Q-2 (Energy Stream)


Connections

Energy Streams

Connection ValueIn [Btu/h] /cooler.OutQ 5942071.9447Out [Btu/h] ---- 5942071.9447



Prepared by:

/catalytic_reactor (Conv Reactor)


Connections

Material Inlets

Connection Up Stream Unit OpIn stream_B heater

Material Outlets

Connection Down Stream Unit OpOut stream_C cooler

Energy Streams

Connection ValueOutQ [Btu/h] ---- -1630754.6084

Summary / Main Data

OutQ [Btu/h] -1630754.6084 Delta P [psi] 0.00Rxn0_Conversion [Fraction] 0.1500

Summary / Configuration

Split Phases False

Material

In OutVapFrac 1.00 1.00T [F] 800.00 800.00P [psia] 14.692 14.692Mole Flow [lbmol/h] 100.00 160.00Mass Flow [lb/h] 10020.19 10020.19Energy [Btu/h] 5551142.6423 5753508.1162Mole Fraction [Fraction] n-HEPTANE 1.00 0.5313 TOLUENE 0.00 0.0938 HYDROGEN 0.00 0.3750Mass Fraction [Fraction] n-HEPTANE 1.00 0.8500 TOLUENE 0.00 0.1379 HYDROGEN 0.00 0.0121MoleFlows [lbmol/h] n-HEPTANE 100.00 85.00 TOLUENE 0.00 15.00 HYDROGEN 0.00 60.00MassFlows [lb/h] n-HEPTANE 10020.19 8517.16 TOLUENE 0.00 1382.08 HYDROGEN 0.00 120.95

Settings / Settings



Prepared by:

Liquid Ports 1 Q Exothermic Is Positive True

Settings / Phase Settings

Liquid Ports 1 Add Solid Port False

Reactions

Rxn0Rxn Name Rxn_1Base Comp n-HEPTANERxn0_Conversion [Fraction] 0.1500Solution Order 0n-HEPTANE -1TOLUENE 1HYDROGEN 4Balance 0.000H Rx'n(25C) [Btu/lbmol] 102321.96



Prepared by:

/cooler (Cooler)


OutQ [Btu/h]Delta P [psi]

OutQ [Btu/h] ---- -1630754.6084

Material

In OutVapFrac 1.00 0.3916T [F] 800.00 65.00P [psia] 14.692 14.692Mole Flow [lbmol/h] 160.00 160.00Mass Flow [lb/h] 10020.19 10020.19Energy [Btu/h] 5753508.1162 -188563.8285Mole Fraction [Fraction] n-HEPTANE 0.5313 0.5313 TOLUENE 0.0938 0.0938 HYDROGEN 0.3750 0.3750Mass Fraction [Fraction] n-HEPTANE 0.8500 0.8500 TOLUENE 0.1379 0.1379 HYDROGEN 0.0121 0.0121MoleFlows [lbmol/h] n-HEPTANE 85.00 85.00 TOLUENE 15.00 15.00 HYDROGEN 60.00 60.00MassFlows [lb/h] n-HEPTANE 8517.16 8517.16 TOLUENE 1382.08 1382.08 HYDROGEN 120.95 120.95



Prepared by:

/heater (Heater)


InQ [Btu/h]Delta P [psi]

OutQ [Btu/h] ---- -1630754.6084

Material

In OutVapFrac 0.00 1.00T [F] 65.00 800.00P [psia] 14.692 14.692Mole Flow [lbmol/h] 100.00 100.00Mass Flow [lb/h] 10020.19 10020.19Energy [Btu/h] -333662.9581 5551142.6423Mole Fraction [Fraction] n-HEPTANE 1.00 1.00 TOLUENE 0.00 0.00 HYDROGEN 0.00 0.00Mass Fraction [Fraction] n-HEPTANE 1.00 1.00 TOLUENE 0.00 0.00 HYDROGEN 0.00 0.00MoleFlows [lbmol/h] n-HEPTANE 100.00 100.00 TOLUENE 0.00 0.00 HYDROGEN 0.00 0.00MassFlows [lb/h] n-HEPTANE 10020.19 10020.19 TOLUENE 0.00 0.00 HYDROGEN 0.00 0.00



Prepared by:

/separator (Separator)


Connections

Material Inlets

Connection Up Stream Unit OpIn stream_D cooler

Material Outlets

Connection Down Stream Unit OpLiq0 stream_F ----Vap stream_E ----

Material

In Liq0 VapVapFrac 0.3916 0.00 1.00T [F] 65.00 65.00 65.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 160.00 97.35 62.65Mass Flow [lb/h] 10020.19 9631.43 388.77Energy [Btu/h] -188563.8285 -425572.3471 237008.5163Mole Fraction [Fraction] n-HEPTANE 0.5313 0.8488 0.0378 TOLUENE 0.0938 0.1507 0.0053 HYDROGEN 0.3750 5.18E-04 0.9569Mass Fraction [Fraction] n-HEPTANE 0.8500 0.8597 0.6106 TOLUENE 0.1379 0.1403 0.0785 HYDROGEN 0.0121 1.06E-05 0.3109MoleFlows [lbmol/h] n-HEPTANE 85.00 82.63 2.37 TOLUENE 15.00 14.67 0.33 HYDROGEN 60.00 0.05 59.95MassFlows [lb/h] n-HEPTANE 8517.16 8279.78 237.38 TOLUENE 1382.08 1351.54 30.54 HYDROGEN 120.95 0.10 120.85

Settings / Settings

Order Liq. Phases by Key Cmp True Key Cmp. in 2nd Liquid WATERMin Key Cmp. in 2nd Liquid [Fraction] 0.5000


simulation repor1 lab 3

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